Chemical Properties of Hexadecane (CAS 544-76-3)

InChI

InChI=1S/C16H34/c1-3-5-7-9-11-13-15-16-14-12-10-8-6-4-2/h3-16H2,1-2H3

InChI Key

DCAYPVUWAIABOU-UHFFFAOYSA-N

Formula

C16H34

SMILES

CCCCCCCCCCCCCCCC

Molecular Weight¹

226.44

CAS

544-76-3

Other Names

• CETANE
• N-CETANE
• n-Hexadecane

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH° : Enthalpy of sublimation at standard conditions (kJ/mol).
• Δ_subH : Enthalpy of sublimation at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_fus : Melting point (K).
• V_c : Critical Volume (m³/kmol).
• v_spec : Specific Volume (m³/kg).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.7420		KDB
ΔcH°liquid	[-10699.10; -10699.10]	kJ/mol
ΔcH°liquid	-10699.10 ± 1.80	kJ/mol	NIST
ΔcH°liquid	-10699.10 ± 4.10	kJ/mol	NIST
ΔfG°	83.74	kJ/mol	KDB
Rg	8.3180		KDB
ΔfH°gas	[-374.90; -373.60]	kJ/mol
ΔfH°gas	-373.60	kJ/mol	KDB
ΔfH°gas	-374.90	kJ/mol	NIST
ΔfH°gas	-374.70	kJ/mol	NIST
ΔfH°liquid	[-456.30; -456.10]	kJ/mol
ΔfH°liquid	-456.30 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-456.10 ± 4.10	kJ/mol	NIST
ΔfusH°	50.04	kJ/mol	Silver ...
ΔsubH°	135.10	kJ/mol	NIST
ΔvapH°	[80.60; 81.80]	kJ/mol
ΔvapH°	81.38	kJ/mol	NIST
ΔvapH°	81.80 ± 1.30	kJ/mol	NIST
ΔvapH°	81.40	kJ/mol	NIST
ΔvapH°	81.40	kJ/mol	NIST
ΔvapH°	81.20	kJ/mol	NIST
ΔvapH°	81.40	kJ/mol	NIST
ΔvapH°	81.40 ± 0.40	kJ/mol	NIST
ΔvapH°	81.10	kJ/mol	NIST
ΔvapH°	Outlier 80.60 ± 1.50	kJ/mol	NIST
log10WS	[-8.40; -8.40]
log10WS	-8.40		Aq. Sol...
log10WS	-8.40		Estimat...
logPoct/wat	6.488		Crippen Calculated Property
McVol	236.300	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
Pc	[1400.00; 1401.00]	kPa
Pc	1400.00	kPa	KDB
Pc	1400.00 ± 200.00	kPa	NIST
Pc	1401.00 ± 50.00	kPa	NIST
ρc	[218.97; 226.44]	kg/m3
ρc	226.44 ± 45.29	kg/m3	NIST
ρc	218.97 ± 6.79	kg/m3	NIST
Inp	[268.29; 272.02]
Inp	268.29		NIST
Inp	272.02		NIST
S°gas	778.31	J/mol×K	NIST
S°liquid	[586.18; 626.80]	J/mol×K
S°liquid	586.18	J/mol×K	NIST
S°liquid	626.80	J/mol×K	NIST
Tboil	[543.00; 561.00]	K
Tboil	560.01	K	KDB
Tboil	560.20	K	NIST
Tboil	559.00 ± 2.00	K	NIST
Tboil	559.92 ± 0.20	K	NIST
Tboil	553.00 ± 5.00	K	NIST
Tboil	556.00 ± 6.00	K	NIST
Tboil	561.00 ± 4.00	K	NIST
Tboil	548.00 ± 5.00	K	NIST
Tboil	543.00 ± 8.00	K	NIST
Tboil	547.00 ± 5.00	K	NIST
Tboil	551.00 ± 5.00	K	NIST
Tc	723.00	K	KDB
Tfus	[288.00; 293.00]	K
Tfus	291.34	K	KDB
Tfus	291.17	K	Aq. Sol...
Tfus	291.45	K	Phase d...
Tfus	291.50	K	Experim...
Tfus	291.10	K	Phase e...
Tfus	291.00	K	Determi...
Tfus	291.30	K	Solid L...
Tfus	291.27 ± 0.02	K	NIST
Tfus	291.32 ± 0.20	K	NIST
Tfus	291.19 ± 0.05	K	NIST
Tfus	291.15 ± 0.50	K	NIST
Tfus	291.00 ± 0.30	K	NIST
Tfus	291.33 ± 0.10	K	NIST
Tfus	291.25 ± 0.10	K	NIST
Tfus	290.00 ± 1.66	K	NIST
Tfus	291.00 ± 2.00	K	NIST
Tfus	291.29 ± 0.02	K	NIST
Tfus	291.29 ± 0.02	K	NIST
Tfus	291.30 ± 0.01	K	NIST
Tfus	291.30 ± 0.06	K	NIST
Tfus	291.30 ± 0.04	K	NIST
Tfus	291.31 ± 0.02	K	NIST
Tfus	291.00 ± 2.00	K	NIST
Tfus	290.00 ± 3.00	K	NIST
Tfus	291.21 ± 0.15	K	NIST
Tfus	291.24 ± 0.10	K	NIST
Tfus	291.24 ± 0.20	K	NIST
Tfus	290.80 ± 0.50	K	NIST
Tfus	291.29 ± 0.02	K	NIST
Tfus	291.29 ± 0.01	K	NIST
Tfus	291.24 ± 0.10	K	NIST
Tfus	Outlier 293.00 ± 0.60	K	NIST
Tfus	291.30 ± 0.02	K	NIST
Tfus	291.20 ± 0.60	K	NIST
Tfus	290.40 ± 1.50	K	NIST
Tfus	291.20 ± 0.40	K	NIST
Tfus	291.00 ± 2.00	K	NIST
Tfus	291.33 ± 0.20	K	NIST
Tfus	291.30 ± 0.30	K	NIST
Tfus	290.60 ± 0.50	K	NIST
Tfus	291.29 ± 0.10	K	NIST
Tfus	Outlier 293.00 ± 3.00	K	NIST
Tfus	292.40 ± 0.50	K	NIST
Tfus	290.20 ± 2.00	K	NIST
Tfus	291.00 ± 0.60	K	NIST
Tfus	Outlier 288.00 ± 3.00	K	NIST
Tfus	291.05 ± 0.40	K	NIST
Tfus	290.10 ± 0.50	K	NIST
Tfus	290.98 ± 0.30	K	NIST
Tfus	Outlier 288.69 ± 2.00	K	NIST
Tfus	290.70 ± 2.00	K	NIST
Tfus	291.26 ± 0.20	K	NIST
Tfus	290.00 ± 2.00	K	NIST
Tfus	291.26 ± 0.20	K	NIST
Tfus	291.00 ± 2.00	K	NIST
Tfus	Outlier 293.00 ± 2.00	K	NIST
Tfus	Outlier 293.00 ± 2.00	K	NIST
Tfus	291.40 ± 2.00	K	NIST
Tfus	292.00 ± 3.00	K	NIST
Tfus	291.00 ± 3.00	K	NIST
Tfus	291.00 ± 2.00	K	NIST
Vc	[1.034; 1.034]	m3/kmol
Vc	1.034	m3/kmol	KDB
Vc	1.034	m3/kmol	NIST
Zc	0.2408100		KDB
Zra	0.24		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[611.73; 715.97]	J/mol×K	[565.48; 724.21]
Cp,gas	611.73	J/mol×K	565.48	Joback Calculated Property
Cp,gas	630.89	J/mol×K	591.94	Joback Calculated Property
Cp,gas	649.30	J/mol×K	618.39	Joback Calculated Property
Cp,gas	667.00	J/mol×K	644.85	Joback Calculated Property
Cp,gas	684.00	J/mol×K	671.30	Joback Calculated Property
Cp,gas	700.31	J/mol×K	697.76	Joback Calculated Property
Cp,gas	715.97	J/mol×K	724.21	Joback Calculated Property
Cp,liquid	[484.90; 512.37]	J/mol×K	[297.79; 313.15]
Cp,liquid	499.00	J/mol×K	297.79	NIST
Cp,liquid	498.30	J/mol×K	298.00	NIST
Cp,liquid	504.20	J/mol×K	298.15	NIST
Cp,liquid	499.62	J/mol×K	298.15	NIST
Cp,liquid	500.21	J/mol×K	298.15	NIST
Cp,liquid	500.21	J/mol×K	298.15	NIST
Cp,liquid	499.62	J/mol×K	298.15	NIST
Cp,liquid	495.73	J/mol×K	298.15	NIST
Cp,liquid	496.45	J/mol×K	298.15	NIST
Cp,liquid	497.16	J/mol×K	298.15	NIST
Cp,liquid	499.97	J/mol×K	298.15	NIST
Cp,liquid	501.60	J/mol×K	298.15	NIST
Cp,liquid	499.72	J/mol×K	298.15	NIST
Cp,liquid	504.58	J/mol×K	298.15	NIST
Cp,liquid	501.45	J/mol×K	298.15	NIST
Cp,liquid	484.90	J/mol×K	311.00	NIST
Cp,liquid	512.37	J/mol×K	313.15	NIST
η	[0.0001705; 0.0034910]	Pa×s	[293.15; 573.15]
η	0.0034910	Pa×s	293.15	Viscome...
η	0.0034860	Pa×s	293.15	Liquid ...
η	0.0030940	Pa×s	298.15	Viscome...
η	0.0030410	Pa×s	298.15	Studies...
η	0.0030410	Pa×s	298.15	Volumet...
η	0.0030410	Pa×s	298.15	Tempera...
η	0.0027060	Pa×s	303.15	Tempera...
η	0.0027060	Pa×s	303.15	Volumet...
η	0.0027780	Pa×s	303.15	Viscome...
η	0.0027720	Pa×s	303.15	Liquid ...
η	0.0027060	Pa×s	303.15	Studies...
η	0.0024090	Pa×s	308.15	Volumet...
η	0.0024090	Pa×s	308.15	Studies...
η	0.0024090	Pa×s	308.15	Tempera...
η	0.0022610	Pa×s	313.15	Liquid ...
η	0.0018400	Pa×s	323.15	Liquid ...
η	0.0012360	Pa×s	348.15	Liquid ...
η	0.0008927	Pa×s	373.15	Liquid ...
η	0.0006788	Pa×s	398.15	Liquid ...
η	0.0005351	Pa×s	423.15	Liquid ...
η	0.0004256	Pa×s	448.15	Liquid ...
η	0.0003440	Pa×s	473.15	Liquid ...
η	0.0002862	Pa×s	498.15	Liquid ...
η	0.0002360	Pa×s	523.15	Liquid ...
η	0.0001937	Pa×s	548.15	Liquid ...
η	0.0001705	Pa×s	573.15	Liquid ...
ΔfusH	[47.55; 53.36]	kJ/mol	[290.70; 292.10]
ΔfusH	53.00	kJ/mol	290.70	NIST
ΔfusH	51.46	kJ/mol	291.10	NIST
ΔfusH	51.46	kJ/mol	291.10	NIST
ΔfusH	51.54	kJ/mol	291.10	NIST
ΔfusH	53.35	kJ/mol	291.30	NIST
ΔfusH	53.36	kJ/mol	291.34	NIST
ΔfusH	47.55	kJ/mol	292.10	NIST
ΔsubH	[80.00; 134.90]	kJ/mol	[288.00; 291.00]
ΔsubH	80.00 ± 3.00	kJ/mol	288.00	NIST
ΔsubH	83.00 ± 8.00	kJ/mol	289.00	NIST
ΔsubH	134.90	kJ/mol	291.00	NIST
ΔvapH	[51.21; 93.40]	kJ/mol	[300.50; 560.50]
ΔvapH	80.20	kJ/mol	300.50	NIST
ΔvapH	93.40	kJ/mol	311.50	NIST
ΔvapH	66.90	kJ/mol	343.00	NIST
ΔvapH	72.90	kJ/mol	349.80	Synthes...
ΔvapH	74.50	kJ/mol	353.00	Express...
ΔvapH	66.20	kJ/mol	353.00	NIST
ΔvapH	65.60	kJ/mol	363.00	NIST
ΔvapH	64.90	kJ/mol	373.00	NIST
ΔvapH	74.90	kJ/mol	373.00	NIST
ΔvapH	64.20	kJ/mol	383.00	NIST
ΔvapH	65.70	kJ/mol	455.50	NIST
ΔvapH	68.50	kJ/mol	488.00	NIST
ΔvapH	61.70	kJ/mol	515.00	NIST
ΔvapH	59.80	kJ/mol	547.00	NIST
ΔvapH	51.21	kJ/mol	560.50	KDB
Pvap	[6.01e-05; 102.04]	kPa	[284.15; 560.90]
Pvap	6.01e-05	kPa	284.15	Determi...
Pvap	1.02e-04	kPa	289.15	Determi...
Pvap	1.68e-04	kPa	294.15	Determi...
Pvap	2.74e-04	kPa	299.15	Determi...
Pvap	4.40e-04	kPa	304.15	Determi...
Pvap	6.96e-04	kPa	309.15	Determi...
Pvap	1.08e-03	kPa	314.15	Determi...
Pvap	1.66e-03	kPa	319.15	Determi...
Pvap	2.52e-03	kPa	324.15	Determi...
Pvap	3.77e-03	kPa	329.15	Determi...
Pvap	5.58e-03	kPa	334.15	Determi...
Pvap	8.16e-03	kPa	339.15	Determi...
Pvap	0.01	kPa	344.15	Determi...
Pvap	0.02	kPa	349.15	Determi...
Pvap	0.02	kPa	354.15	Determi...
Pvap	0.03	kPa	359.15	Determi...
Pvap	0.05	kPa	364.15	Determi...
Pvap	0.06	kPa	369.15	Determi...
Pvap	0.09	kPa	374.15	Determi...
Pvap	0.12	kPa	379.15	Determi...
Pvap	0.16	kPa	384.15	Determi...
Pvap	0.21	kPa	389.15	Determi...
Pvap	0.28	kPa	394.15	Determi...
Pvap	0.37	kPa	399.15	Determi...
Pvap	0.48	kPa	404.15	Determi...
Pvap	0.63	kPa	409.15	Determi...
Pvap	0.81	kPa	414.15	Determi...
Pvap	1.03	kPa	419.15	Determi...
Pvap	1.32	kPa	424.15	Determi...
Pvap	1.67	kPa	429.15	Determi...
Pvap	2.10	kPa	434.15	Determi...
Pvap	2.63	kPa	439.15	Determi...
Pvap	3.28	kPa	444.15	Determi...
Pvap	4.07	kPa	449.15	Determi...
Pvap	5.02	kPa	454.15	Determi...
Pvap	6.18	kPa	459.15	Determi...
Pvap	7.56	kPa	464.15	Determi...
Pvap	9.21	kPa	469.15	Determi...
Pvap	11.20	kPa	474.15	Determi...
Pvap	13.50	kPa	479.15	Determi...
Pvap	16.30	kPa	484.15	Determi...
Pvap	14.78	kPa	486.10	Vapor p...
Pvap	19.50	kPa	489.15	Determi...
Pvap	23.30	kPa	494.15	Determi...
Pvap	27.70	kPa	499.15	Determi...
Pvap	32.90	kPa	504.15	Determi...
Pvap	38.90	kPa	509.15	Determi...
Pvap	49.76	kPa	529.60	Vapor p...
Pvap	79.60	kPa	549.30	Vapor p...
Pvap	101.35	kPa	560.50	Vapor p...
Pvap	102.04	kPa	560.90	Vapor p...
n0	[1.41450; 1.43520]		[293.10; 343.15]
n0	1.43440		293.10	Liquid-...
n0	1.43520		293.15	Densiti...
n0	1.43460		293.15	Experim...
n0	1.43232		298.15	Phase b...
n0	1.43230		298.15	Measure...
n0	1.43250		298.15	Liquid-...
n0	1.43250		298.15	Liquid-...
n0	1.43400		298.15	Densiti...
n0	1.43232		298.15	Thiophe...
n0	1.43180		298.20	Liquid-...
n0	1.43110		303.15	Densiti...
n0	1.42690		313.15	Densiti...
n0	1.42280		323.15	Densiti...
n0	1.41870		333.15	Densiti...
n0	1.41450		343.15	Densiti...
ρl	[717.50; 773.70]	kg/m3	[293.00; 373.15]
ρl	773.00	kg/m3	293.00	KDB
ρl	773.50	kg/m3	293.15	Liquid-...
ρl	773.33	kg/m3	293.15	Densiti...
ρl	773.37	kg/m3	293.15	Densiti...
ρl	773.70	kg/m3	293.15	Density...
ρl	773.49	kg/m3	293.15	Density...
ρl	773.42	kg/m3	293.15	Density...
ρl	769.91	kg/m3	298.15	Thermod...
ρl	769.87	kg/m3	298.15	A syste...
ρl	770.22	kg/m3	298.15	Thermod...
ρl	771.50	kg/m3	298.15	Ternary...
ρl	771.15	kg/m3	298.15	Solvent...
ρl	770.31	kg/m3	298.15	Excess ...
ρl	770.22	kg/m3	298.15	Liquid ...
ρl	770.31	kg/m3	298.15	Excess ...
ρl	770.31	kg/m3	298.15	Excess ...
ρl	773.19	kg/m3	298.15	Binary ...
ρl	769.92	kg/m3	298.15	Measure...
ρl	770.22	kg/m3	298.15	Liquid ...
ρl	770.30	kg/m3	298.15	Liquid ...
ρl	770.21	kg/m3	298.15	Liquid-...
ρl	770.14	kg/m3	298.15	Liquid-...
ρl	773.19	kg/m3	298.15	(Liquid...
ρl	769.86	kg/m3	298.15	Densiti...
ρl	770.32	kg/m3	298.15	Thermod...
ρl	769.93	kg/m3	298.15	Liquid-...
ρl	769.81	kg/m3	298.15	Densiti...
ρl	770.01	kg/m3	298.15	Liquid-...
ρl	769.89	kg/m3	298.15	Densiti...
ρl	770.30	kg/m3	298.20	Ternary...
ρl	766.47	kg/m3	303.15	Density...
ρl	766.55	kg/m3	303.15	Density...
ρl	766.40	kg/m3	303.15	Densiti...
ρl	766.80	kg/m3	303.15	Density...
ρl	766.40	kg/m3	303.15	A syste...
ρl	766.51	kg/m3	303.15	Measure...
ρl	766.43	kg/m3	303.15	Densiti...
ρl	762.95	kg/m3	308.15	A syste...
ρl	762.94	kg/m3	308.15	Densiti...
ρl	763.06	kg/m3	308.15	Measure...
ρl	762.89	kg/m3	308.15	Densiti...
ρl	759.60	kg/m3	313.15	Measure...
ρl	759.63	kg/m3	313.15	Density...
ρl	759.55	kg/m3	313.15	Experim...
ρl	759.51	kg/m3	313.15	Densiti...
ρl	759.48	kg/m3	313.15	Densiti...
ρl	759.55	kg/m3	313.15	Density...
ρl	762.90	kg/m3	313.15	Excess ...
ρl	759.90	kg/m3	313.15	Density...
ρl	755.98	kg/m3	318.15	Densiti...
ρl	755.99	kg/m3	318.15	Densiti...
ρl	756.14	kg/m3	318.15	Measure...
ρl	752.63	kg/m3	323.15	Density...
ρl	752.90	kg/m3	323.15	Density...
ρl	752.58	kg/m3	323.15	Densiti...
ρl	752.64	kg/m3	323.15	Experim...
ρl	752.68	kg/m3	323.15	Measure...
ρl	752.71	kg/m3	323.15	Density...
ρl	752.60	kg/m3	323.15	Densiti...
ρl	746.00	kg/m3	333.15	Density...
ρl	745.71	kg/m3	333.15	Density...
ρl	745.69	kg/m3	333.15	Densiti...
ρl	745.79	kg/m3	333.15	Density...
ρl	745.73	kg/m3	333.15	Experim...
ρl	739.00	kg/m3	343.15	Density...
ρl	738.80	kg/m3	343.15	Density...
ρl	738.90	kg/m3	343.15	Density...
ρl	731.80	kg/m3	353.15	Density...
ρl	731.90	kg/m3	353.15	Density...
ρl	724.70	kg/m3	363.15	Density...
ρl	724.80	kg/m3	363.15	Density...
ρl	717.70	kg/m3	373.15	Density...
ρl	717.50	kg/m3	373.15	Density...
ΔfusS	[176.79; 183.15]	J/mol×K	[291.10; 291.34]
ΔfusS	177.10	J/mol×K	291.10	NIST
ΔfusS	176.79	J/mol×K	291.10	NIST
ΔfusS	183.13	J/mol×K	291.30	NIST
ΔfusS	183.15	J/mol×K	291.34	NIST
csound,fluid	[1074.00; 1367.20]	m/s	[290.65; 373.15]
csound,fluid	1367.20	m/s	290.65	Density...
csound,fluid	1365.30	m/s	291.15	Density...
csound,fluid	1363.40	m/s	291.65	Density...
csound,fluid	1361.50	m/s	292.15	Density...
csound,fluid	1359.60	m/s	292.65	Density...
csound,fluid	1356.00	m/s	293.00	Fixed-P...
csound,fluid	1357.70	m/s	293.15	Density...
csound,fluid	1357.40	m/s	293.15	Densiti...
csound,fluid	1357.00	m/s	293.15	Tempera...
csound,fluid	1340.00	m/s	298.00	Fixed-P...
csound,fluid	1338.00	m/s	298.15	Tempera...
csound,fluid	1338.80	m/s	298.15	Density...
csound,fluid	1325.00	m/s	303.00	Fixed-P...
csound,fluid	1320.20	m/s	303.15	Density...
csound,fluid	1319.60	m/s	303.15	Densiti...
csound,fluid	1312.00	m/s	303.15	Tempera...
csound,fluid	1301.70	m/s	308.15	Density...
csound,fluid	1301.00	m/s	308.15	Tempera...
csound,fluid	1287.00	m/s	313.00	Fixed-P...
csound,fluid	1283.40	m/s	313.15	Density...
csound,fluid	1283.00	m/s	313.15	Tempera...
csound,fluid	1282.90	m/s	313.15	Densiti...
csound,fluid	1268.00	m/s	318.00	Fixed-P...
csound,fluid	1265.00	m/s	318.15	Tempera...
csound,fluid	1265.30	m/s	318.15	Density...
csound,fluid	1248.00	m/s	323.00	Fixed-P...
csound,fluid	1246.00	m/s	323.15	Tempera...
csound,fluid	1247.40	m/s	323.15	Density...
csound,fluid	1247.00	m/s	323.15	Densiti...
csound,fluid	1227.00	m/s	328.00	Fixed-P...
csound,fluid	1228.00	m/s	328.15	Tempera...
csound,fluid	1229.80	m/s	328.15	Density...
csound,fluid	1210.00	m/s	333.00	Fixed-P...
csound,fluid	1212.30	m/s	333.15	Density...
csound,fluid	1211.00	m/s	333.15	Tempera...
csound,fluid	1212.10	m/s	333.15	Densiti...
csound,fluid	1194.90	m/s	338.15	Density...
csound,fluid	1193.00	m/s	338.15	Tempera...
csound,fluid	1176.00	m/s	343.15	Tempera...
csound,fluid	1177.90	m/s	343.15	Density...
csound,fluid	1158.00	m/s	348.15	Tempera...
csound,fluid	1141.00	m/s	353.15	Tempera...
csound,fluid	1124.00	m/s	358.15	Tempera...
csound,fluid	1107.00	m/s	363.15	Tempera...
csound,fluid	1090.00	m/s	368.15	Tempera...
csound,fluid	1074.00	m/s	373.15	Tempera...
γ	[0.03; 0.03]	N/m	[294.00; 313.20]
γ	0.03	N/m	294.00	Densiti...
γ	0.03	N/m	294.80	Density...
γ	0.03	N/m	313.20	KDB
vspec	[0.00; 0.00]	m3/kg	[298.00; 573.00]
vspec	0.00	m3/kg	298.00	A simpl...
vspec	0.00	m3/kg	323.00	A simpl...
vspec	0.00	m3/kg	348.00	A simpl...
vspec	0.00	m3/kg	373.00	A simpl...
vspec	0.00	m3/kg	398.00	A simpl...
vspec	0.00	m3/kg	423.00	A simpl...
vspec	0.00	m3/kg	448.00	A simpl...
vspec	0.00	m3/kg	473.00	A simpl...
vspec	0.00	m3/kg	498.00	A simpl...
vspec	0.00	m3/kg	523.00	A simpl...
vspec	0.00	m3/kg	548.00	A simpl...
vspec	0.00	m3/kg	573.00	A simpl...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[444.06; 496.42]	K	[3.47; 22.39]
Tboil	444.06	K	3.47	Improvi...
Tboil	474.05	K	10.37	Improvi...
Tboil	486.81	K	15.17	Improvi...
Tboil	493.60	K	18.66	Improvi...
Tboil	496.42	K	22.39	Improvi...
Tfus	[291.50; 343.15]	K	[100.00; 251030.00]
Tfus	291.50	K	100.00	Liquid ...
Tfus	293.15	K	9210.00	Influen...
Tfus	293.15	K	9210.00	High pr...
Tfus	296.00	K	20000.00	Liquid ...
Tfus	300.40	K	40000.00	Liquid ...
Tfus	303.15	K	50650.00	High pr...
Tfus	303.15	K	50650.00	Influen...
Tfus	304.80	K	60000.00	Liquid ...
Tfus	309.70	K	80000.00	Liquid ...
Tfus	313.15	K	95560.00	Influen...
Tfus	313.15	K	95560.00	High pr...
Tfus	313.50	K	100000.00	Liquid ...
Tfus	323.15	K	143920.00	Influen...
Tfus	323.15	K	143920.00	High pr...
Tfus	333.15	K	195740.00	High pr...
Tfus	333.15	K	195740.00	Influen...
Tfus	343.15	K	251030.00	High pr...
Tfus	343.15	K	251030.00	Influen...

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (3)
3. Mass density, kg/m3 (6)

Molar heat capacity at constant pressure, J/K/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
323.15	130.00	513.57
328.15	130.00	517.19
333.15	130.00	520.81
338.15	130.00	524.66
343.15	130.00	528.51
348.15	130.00	532.82
353.15	130.00	536.44
358.15	130.00	540.74
363.15	130.00	544.59
368.15	130.00	548.67
373.15	130.00	553.20
378.15	130.00	557.27
383.15	130.00	561.57
388.15	130.00	565.65
393.15	130.00	569.73
398.15	130.00	574.03
403.15	130.00	578.56
408.15	130.00	583.09
413.15	130.00	586.94
418.15	130.00	591.46
423.15	130.00	595.77
428.15	130.00	599.62
433.15	130.00	603.92
438.15	130.00	608.67
443.15	130.00	613.20
448.15	130.00	617.28
453.15	130.00	622.26
323.15	10090.00	512.21
328.15	10090.00	515.83
333.15	10090.00	519.46
338.15	10090.00	523.31
343.15	10090.00	526.48
348.15	10090.00	530.10
353.15	10090.00	534.40
358.15	10090.00	538.48
363.15	10090.00	542.10
368.15	10090.00	546.40
373.15	10090.00	550.70
378.15	10090.00	554.55
383.15	10090.00	558.86
388.15	10090.00	563.16
393.15	10090.00	567.24
398.15	10090.00	571.31
403.15	10090.00	575.61
408.15	10090.00	579.92
413.15	10090.00	584.44
418.15	10090.00	588.97
423.15	10090.00	593.05
428.15	10090.00	596.45
433.15	10090.00	600.30
438.15	10090.00	604.60
443.15	10090.00	609.35
448.15	10090.00	613.66
453.15	10090.00	617.05
458.15	10090.00	621.35
463.15	10090.00	625.43
468.15	10090.00	630.19
473.15	10090.00	634.94
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.90	3300.00	0.0028
303.90	7300.00	0.0030
303.90	12900.00	0.0032
303.90	19000.00	0.0035
303.90	26800.00	0.0038
303.90	33600.00	0.0041
325.70	8100.00	0.0019
325.70	8300.00	0.0020
325.70	21500.00	0.0023
325.70	35600.00	0.0027
325.70	49300.00	0.0031
325.70	63600.00	0.0036
325.70	77500.00	0.0041
325.70	91800.00	0.0046
325.70	104100.00	0.0052
325.70	119200.00	0.0059
325.70	122700.00	0.0061
429.10	12800.00	0.0006
429.10	12800.00	0.0006
429.10	22200.00	0.0006
429.10	22700.00	0.0006
429.10	35800.00	0.0007
429.10	70500.00	0.0010
429.10	91600.00	0.0012
429.10	118800.00	0.0014
429.10	140300.00	0.0016
429.10	167800.00	0.0018
429.10	188000.00	0.0020
429.10	222900.00	0.0025
533.70	14100.00	0.0003
533.70	14300.00	0.0003
533.70	29900.00	0.0003
533.70	30100.00	0.0003
533.70	50400.00	0.0004
533.70	50500.00	0.0004
533.70	77100.00	0.0005
533.70	104600.00	0.0006
533.70	125000.00	0.0007
533.70	152800.00	0.0008
533.70	188400.00	0.0010
533.70	210000.00	0.0011
533.70	226600.00	0.0012
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
323.70	970.00	0.0019
322.70	1940.00	0.0019
323.80	1980.00	0.0019
323.70	3000.00	0.0019
323.80	3910.00	0.0019
372.70	990.00	0.0009
372.70	1960.00	0.0009
372.80	2970.00	0.0009
372.80	3950.00	0.0009
373.90	980.00	0.0009
373.90	2000.00	0.0009
373.90	2980.00	0.0009
373.90	3900.00	0.0009
422.90	1990.00	0.0006
422.90	2970.00	0.0006
422.90	3840.00	0.0006
471.90	1000.00	0.0004
472.00	2010.00	0.0004
472.10	2910.00	0.0004
472.10	3870.00	0.0004
473.70	3990.00	0.0004
521.90	970.00	0.0002
521.90	1960.00	0.0003
521.90	2950.00	0.0003
522.00	3830.00	0.0003
572.20	2000.00	0.0002
572.10	2930.00	0.0002
572.20	3850.00	0.0002
621.90	2010.00	0.0001
622.00	2890.00	0.0001
622.10	3820.00	0.0001
623.20	3990.00	0.0001
673.20	2000.00	0.0001
673.60	3000.00	0.0001
672.60	3990.00	0.0001
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
318.15	6895.00	0.0022
318.15	13790.00	0.0023
318.15	20680.00	0.0025
318.15	27580.00	0.0027
318.15	34470.00	0.0029
318.15	41370.00	0.0032
318.15	48260.00	0.0034
318.15	55160.00	0.0036
318.15	62050.00	0.0039
333.15	6895.00	0.0017
333.15	13790.00	0.0018
333.15	20680.00	0.0020
333.15	27580.00	0.0021
333.15	34470.00	0.0022
333.15	41370.00	0.0024
333.15	48260.00	0.0026
333.15	55160.00	0.0028
333.15	62050.00	0.0030
348.15	6895.00	0.0013
348.15	13790.00	0.0014
348.15	20680.00	0.0016
348.15	27580.00	0.0017
348.15	34470.00	0.0018
348.15	41370.00	0.0019
348.15	48260.00	0.0021
348.15	55160.00	0.0022
348.15	62050.00	0.0024
363.15	6895.00	0.0011
363.15	13790.00	0.0012
363.15	20680.00	0.0013
363.15	27580.00	0.0014
363.15	34470.00	0.0015
363.15	41370.00	0.0016
363.15	48260.00	0.0017
363.15	55160.00	0.0018
363.15	62050.00	0.0019
388.15	6895.00	0.0008
388.15	13790.00	0.0009
388.15	20680.00	0.0010
388.15	27580.00	0.0010
388.15	34470.00	0.0012
388.15	41370.00	0.0012
388.15	48260.00	0.0013
388.15	55160.00	0.0013
388.15	62050.00	0.0014
413.15	6895.00	0.0006
413.15	13790.00	0.0007
413.15	20680.00	0.0007
413.15	27580.00	0.0008
413.15	34470.00	0.0008
413.15	41370.00	0.0009
413.15	48260.00	0.0009
413.15	55160.00	0.0010
413.15	62050.00	0.0010
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
323.65	14900.00	758.0
323.65	27900.00	769.0
323.65	41500.00	779.0
323.65	55500.00	787.0
323.65	69400.00	792.0
323.65	81300.00	799.0
323.65	109700.00	807.0
422.85	14100.00	700.0
422.85	27900.00	713.0
422.85	41200.00	724.0
422.85	55500.00	734.0
422.85	69800.00	743.0
422.85	82800.00	750.0
422.85	108800.00	765.0
422.85	136900.00	778.0
422.85	170700.00	792.0
422.85	204300.00	804.0
422.85	236500.00	815.0
422.85	262300.00	823.0
522.55	15100.00	643.0
522.55	27100.00	660.0
522.55	42000.00	675.0
522.55	55400.00	687.0
522.55	69100.00	698.0
522.55	82100.00	707.0
522.55	107900.00	723.0
522.55	135800.00	738.0
522.55	170100.00	755.0
522.55	203300.00	769.0
522.55	235800.00	782.0
522.55	255000.00	788.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	769.98
313.15	100.00	759.6
333.15	100.00	745.81
373.15	100.00	717.79
393.15	100.00	703.59
433.15	100.00	674.64
298.15	10100.00	776.41
313.15	10100.00	766.44
373.15	10100.00	727.21
393.15	10100.00	714.02
433.15	10100.00	687.77
298.15	20100.00	782.34
313.15	20100.00	772.76
333.15	20100.00	760.5
373.15	20100.00	735.47
393.15	20100.00	723.09
433.15	20100.00	698.82
313.15	30100.00	778.65
373.15	30100.00	742.97
313.15	40100.00	784.24
333.15	40100.00	773.01
373.15	40100.00	749.88
393.15	40100.00	738.85
433.15	40100.00	717.04
333.15	50100.00	778.56
373.15	50100.00	756.25
313.15	60100.00	794.38
333.15	60100.00	783.47
373.15	60100.00	762.2
393.15	60100.00	752.0
433.15	60100.00	731.95
313.15	80100.00	803.42
333.15	80100.00	793.1
373.15	80100.00	773.03
393.15	80100.00	763.28
433.15	80100.00	744.68
333.15	100100.00	801.83
373.15	100100.00	782.74
393.15	100100.00	773.48
433.15	100100.00	755.89
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	770.5
298.15	1000.00	771.1
298.15	5000.00	773.6
298.15	10000.00	776.9
298.15	20000.00	782.6
298.15	30000.00	788.1
323.15	100.00	753.1
323.15	1000.00	753.9
323.15	5000.00	756.8
323.15	10000.00	760.4
323.15	20000.00	766.9
323.15	30000.00	772.9
323.15	40000.00	778.5
323.15	50000.00	783.8
323.15	60000.00	788.7
348.15	100.00	735.6
348.15	1000.00	736.5
348.15	5000.00	739.8
348.15	10000.00	743.8
348.15	20000.00	751.1
348.15	30000.00	757.8
348.15	40000.00	763.9
348.15	50000.00	769.7
348.15	60000.00	775.1
373.15	100.00	717.8
373.15	1000.00	719.4
373.15	5000.00	723.2
373.15	10000.00	727.7
373.15	20000.00	735.9
373.15	30000.00	743.4
373.15	40000.00	750.3
373.15	50000.00	756.5
373.15	60000.00	762.4
423.15	100.00	680.8
423.15	1000.00	684.1
423.15	5000.00	689.2
423.15	10000.00	695.1
423.15	20000.00	705.5
423.15	30000.00	714.7
423.15	40000.00	722.9
423.15	50000.00	730.4
423.15	60000.00	737.2
463.15	100.00	651.6
463.15	1000.00	654.5
463.15	5000.00	661.0
463.15	10000.00	668.5
463.15	20000.00	681.2
463.15	30000.00	692.0
463.15	40000.00	701.4
463.15	50000.00	709.8
463.15	60000.00	717.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.20	10000.00	775.86
303.20	10000.00	773.66
313.20	10000.00	764.59
323.20	10000.00	759.8
333.20	10000.00	753.38
348.20	10000.00	744.11
353.20	10000.00	740.03
373.20	10000.00	727.81
393.20	10000.00	713.25
413.20	10000.00	700.27
423.20	10000.00	694.3
433.20	10000.00	687.01
453.20	10000.00	674.02
463.20	10000.00	669.34
473.20	10000.00	660.45
298.20	20000.00	782.89
303.20	20000.00	779.38
313.20	20000.00	773.09
323.20	20000.00	766.48
333.20	20000.00	760.44
348.20	20000.00	751.32
353.20	20000.00	748.27
373.20	20000.00	736.02
393.20	20000.00	723.64
413.20	20000.00	711.23
423.20	20000.00	705.01
433.20	20000.00	698.74
453.20	20000.00	686.53
463.20	20000.00	680.32
473.20	20000.00	673.95
298.20	30000.00	788.75
303.20	30000.00	785.01
313.20	30000.00	778.81
323.20	30000.00	773.19
333.20	30000.00	767.3
348.20	30000.00	758.67
353.20	30000.00	755.72
373.20	30000.00	744.18
393.20	30000.00	732.3
413.20	30000.00	720.49
423.20	30000.00	714.62
433.20	30000.00	708.69
453.20	30000.00	696.77
463.20	30000.00	690.8
473.20	30000.00	685.23
298.20	40000.00	793.81
303.20	40000.00	790.38
313.20	40000.00	784.36
323.20	40000.00	778.83
333.20	40000.00	773.53
348.20	40000.00	765.1
353.20	40000.00	762.19
373.20	40000.00	751.02
393.20	40000.00	739.4
413.20	40000.00	728.42
423.20	40000.00	722.88
433.20	40000.00	717.4
453.20	40000.00	706.13
463.20	40000.00	700.49
473.20	40000.00	695.19
298.20	50000.00	799.18
303.20	50000.00	795.64
313.20	50000.00	789.46
323.20	50000.00	784.38
333.20	50000.00	779.1
348.20	50000.00	770.98
353.20	50000.00	768.11
373.20	50000.00	757.42
393.20	50000.00	746.41
413.20	50000.00	735.85
423.20	50000.00	730.73
433.20	50000.00	725.14
453.20	50000.00	714.59
463.20	50000.00	709.18
473.20	50000.00	704.05
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
318.15	6895.00	760.3
318.15	13789.00	765.0
318.15	20684.00	769.6
318.15	27579.00	773.9
318.15	34474.00	777.7
318.15	41369.00	781.5
318.15	48263.00	785.2
318.15	55158.00	788.7
318.15	62053.00	791.7
333.15	6895.00	750.7
333.15	13789.00	755.8
333.15	20684.00	760.4
333.15	27579.00	765.1
333.15	34474.00	769.7
333.15	41369.00	773.9
333.15	48263.00	777.6
333.15	55158.00	781.2
333.15	62053.00	784.3
348.15	6895.00	741.7
348.15	13789.00	747.2
348.15	20684.00	752.5
348.15	27579.00	757.2
348.15	34474.00	761.9
348.15	41369.00	766.1
348.15	48263.00	770.2
348.15	55158.00	774.1
348.15	62053.00	777.6
363.15	6895.00	732.0
363.15	13789.00	738.1
363.15	20684.00	743.9
363.15	27579.00	748.6
363.15	34474.00	753.7
363.15	41369.00	758.4
363.15	48263.00	762.6
363.15	55158.00	766.7
363.15	62053.00	770.5
388.15	6895.00	714.7
388.15	13789.00	721.7
388.15	20684.00	728.1
388.15	27579.00	733.9
388.15	34474.00	739.2
388.15	41369.00	744.1
388.15	48263.00	748.8
388.15	55158.00	753.3
388.15	62053.00	757.5
413.15	6895.00	696.2
413.15	13789.00	704.3
413.15	20684.00	711.0
413.15	27579.00	717.9
413.15	34474.00	723.7
413.15	41369.00	729.4
413.15	48263.00	734.5
413.15	55158.00	739.5
413.15	62053.00	743.8
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.15	340.00	759.52
313.15	690.00	759.83
313.15	1030.00	760.08
313.15	1380.00	760.33
313.15	1720.00	760.65
313.15	2070.00	760.88
313.15	2410.00	761.08
313.15	2760.00	761.33
313.15	3100.00	761.65
313.15	3450.00	761.83
313.15	3800.00	762.08
313.15	4140.00	762.33
313.15	4480.00	762.49
313.15	4830.00	762.83
313.15	5170.00	763.08
313.15	5510.00	763.33
313.15	5860.00	763.58
313.15	6200.00	763.83
313.15	6550.00	764.08
313.15	6890.00	764.33
313.15	7240.00	764.65
313.15	7580.00	764.83
313.15	7930.00	765.08
313.15	8270.00	765.33
313.15	8620.00	765.58
313.15	8960.00	765.74
313.15	9310.00	765.99
313.15	9650.00	766.24
313.15	10000.00	766.49
313.15	10340.00	766.74
313.15	10690.00	766.98
313.15	11030.00	767.22
313.15	11380.00	767.48
333.15	340.00	746.8
333.15	690.00	747.1
333.15	1030.00	747.4
333.15	1380.00	747.7
333.15	1720.00	748.0
333.15	2070.00	748.2
333.15	2410.00	748.5
333.15	2760.00	748.7
333.15	3100.00	749.0
333.15	3450.00	749.2
333.15	3800.00	749.5
333.15	4140.00	749.8
333.15	4480.00	750.0
333.15	4830.00	750.2
333.15	5170.00	750.5
333.15	5510.00	750.7
333.15	5860.00	751.0
333.15	6200.00	751.2
333.15	6550.00	751.4
333.15	6890.00	751.6
333.15	7240.00	752.0
333.15	7580.00	752.4
333.15	7930.00	752.6
333.15	8270.00	752.8
333.15	8620.00	753.0
333.15	8960.00	753.2
333.15	9310.00	753.5
333.15	9650.00	753.8
333.15	10000.00	754.0
333.15	10340.00	754.3
333.15	10690.00	754.5
333.15	11030.00	754.8
333.15	11380.00	755.0
353.15	340.00	736.2
353.15	690.00	736.4
353.15	1030.00	736.6
353.15	1380.00	736.9
353.15	1720.00	737.1
353.15	2070.00	737.4
353.15	2410.00	737.7
353.15	2760.00	738.0
353.15	3100.00	738.3
353.15	3450.00	738.7
353.15	3800.00	739.1
353.15	4140.00	739.3
353.15	4480.00	739.5
353.15	4830.00	739.8
353.15	5170.00	740.0
353.15	5510.00	740.2
353.15	5860.00	740.4
353.15	6200.00	740.5
353.15	6550.00	740.7
353.15	6890.00	741.0
353.15	7240.00	741.2
353.15	7580.00	741.5
353.15	7930.00	741.7
353.15	8270.00	742.0
353.15	8620.00	742.2
353.15	8960.00	742.5
353.15	9310.00	742.7
353.15	9650.00	742.9
353.15	10000.00	743.1
353.15	10340.00	743.5
353.15	10690.00	743.9
353.15	11030.00	744.1
353.15	11380.00	744.3
373.15	340.00	723.1
373.15	690.00	723.3
373.15	1030.00	723.6
373.15	1380.00	723.8
373.15	1720.00	724.0
373.15	2070.00	724.3
373.15	2410.00	724.6
373.15	2760.00	724.9
373.15	3100.00	725.1
373.15	3450.00	725.4
373.15	3800.00	725.6
373.15	4140.00	725.9
373.15	4480.00	726.1
373.15	4830.00	726.4
373.15	5170.00	726.7
373.15	5510.00	726.9
373.15	5860.00	727.2
373.15	6200.00	727.5
373.15	6550.00	727.8
373.15	6890.00	728.1
373.15	7240.00	728.4
373.15	7580.00	728.5
373.15	7930.00	728.9
373.15	8270.00	729.4
373.15	8620.00	729.9
373.15	8960.00	730.2
373.15	9310.00	730.6
373.15	9650.00	730.8
373.15	10000.00	731.0
373.15	10340.00	731.4
373.15	10690.00	731.6
373.15	11030.00	731.9
373.15	11380.00	732.1
393.15	340.00	710.0
393.15	690.00	710.3
393.15	1030.00	710.6
393.15	1380.00	710.9
393.15	1720.00	711.1
393.15	2070.00	711.4
393.15	2410.00	711.7
393.15	2760.00	712.0
393.15	3100.00	712.2
393.15	3450.00	712.3
393.15	3800.00	712.5
393.15	4140.00	712.8
393.15	4480.00	713.0
393.15	4830.00	713.3
393.15	5170.00	713.5
393.15	5510.00	713.8
393.15	5860.00	714.0
393.15	6200.00	714.3
393.15	6550.00	714.6
393.15	6890.00	714.9
393.15	7240.00	715.1
393.15	7580.00	715.3
393.15	7930.00	715.5
393.15	8270.00	715.8
393.15	8620.00	716.0
393.15	8960.00	716.3
393.15	9310.00	716.6
393.15	9650.00	716.8
393.15	10000.00	717.1
393.15	10340.00	717.4
393.15	10690.00	717.6
393.15	11030.00	717.9
393.15	11380.00	718.1
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[421.88; 585.67]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.54069e+01
Coefficient B			-4.97629e+03
Coefficient C			-9.27430e+01
Temperature range, min.			421.88
Temperature range, max.			585.67
Pvap	1.33	kPa	421.88	Calculated Property
Pvap	2.94	kPa	440.08	Calculated Property
Pvap	6.01	kPa	458.28	Calculated Property
Pvap	11.46	kPa	476.48	Calculated Property
Pvap	20.61	kPa	494.68	Calculated Property
Pvap	35.24	kPa	512.87	Calculated Property
Pvap	57.63	kPa	531.07	Calculated Property
Pvap	90.61	kPa	549.27	Calculated Property
Pvap	137.62	kPa	567.47	Calculated Property
Pvap	202.65	kPa	585.67	Calculated Property
Pvap	[8.83e-05; 1413.13]	kPa	[291.32; 720.60]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.60137e+02
Coefficient B			-1.55289e+04
Coefficient C			-2.05917e+01
Coefficient D			8.01493e-06
Temperature range, min.			291.32
Temperature range, max.			720.60
Pvap	8.83e-05	kPa	291.32	Calculated Property
Pvap	8.95e-03	kPa	339.02	Calculated Property
Pvap	0.22	kPa	386.72	Calculated Property
Pvap	2.29	kPa	434.41	Calculated Property
Pvap	13.07	kPa	482.11	Calculated Property
Pvap	50.12	kPa	529.81	Calculated Property
Pvap	145.97	kPa	577.51	Calculated Property
Pvap	350.91	kPa	625.20	Calculated Property
Pvap	737.67	kPa	672.90	Calculated Property
Pvap	1413.13	kPa	720.60	Calculated Property

Similar Compounds

Find more compounds similar to Hexadecane.

Mixtures

• n-Hexane + Hexadecane
• Hexadecane + Tetradecane
• Hexadecane + 2,3-Pentanedione
• Hexadecane + Benzaldehyde
• Hexadecane + Octadecane
• Benzene + Hexadecane + Ethanol, 2-methoxy-
• Toluene + Hexadecane + Ethanol, 2-methoxy-
• p-Xylene + Hexadecane + Ethanol, 2-methoxy-
• Benzene + Acetonitrile + Hexadecane
• Toluene + Acetonitrile + Hexadecane
• Acetonitrile + p-Xylene + Hexadecane
• Hexadecane + Acetophenone
• Benzyl methyl ketone + Hexadecane
• Carbon dioxide + Hexadecane
• 1-Propanol + Hexadecane
• Hexadecane + 1-Butanol
• Hexadecane + Pentane, 3-methyl-
• Hexadecane + Butane, 2,2-dimethyl-
• Benzene + Hexadecane
• Isopropyl Alcohol + Hexadecane

Find more mixtures with Hexadecane.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
• Excess Volumes, Densities, Speeds of Sound, and Viscosities for the Binary Systems of 1-Octanol with Hexadecane and Squalane at (298.15, 303.15 and 308.15) K
• High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
• Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
• Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems
• Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
• Measurement and correlation of liquid liquid equilibria for acetonitrile + n-alkane systems
• Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
• Viscometric and volumetric behaviour of binary mixtures of sulfolane and N-methylpyrrolidone with monoethanolamine and diethanolamine in the range 303 373 K
• Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
• Ionic liquids on desulfurization of fuel oils
• Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
• Separation of propylbenzene and n-alkanes from their mixtures using 4-methyl-N-butylpyridinium tetrafluoroborate as an ionic solvent at several temperatures
• Experimental measurements and equation of state modeling of liquid densities for long-chain n-alkanes at pressures to 265 MPa and temperatures to 523 K
• Liquid-liquid equilibria for the ternary system (water + hexadecane + dipropylene glycol n-propyl ether)
• Liquid-liquid equilibria for ternary systems acetic acid + n-butylacetate + hydrocarbons at 293.15 K
• Liquid-liquid equilibria for benzaldehyde + n-alkane mixtures andcharacterization of benzaldehyde + hydrocarbon systems in terms of DISQUAC
• A modified continuous flow apparatus for gas solubility measurements at high pressure and temperature with camera system
• Experimental measurements and thermodynamic modeling of wax disappearance temperature for the binary systems n-C14H30 + n- C16H34, n-C16H34 + n-C18H38 and n-C11H24 + n-C18H38
• Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
• Liquid liquid equilibria for acetophenone + n-alkane mixtures and characterization of acetophenone systems using DISQUAC
• Speed of sound and thermodynamic properties of ternary liquid mixture octane + dodecane + hexadecane
• Extraction of nitrogen compounds from diesel fuel using imidazolium- and pyridinium- based ionic liquids: Experiments, COSMO-RS prediction and NRTL correlation
• Isobaric vapor-liquid equilibrium for the three binary systems of C14 - C16 n-alkane + methyl myristate at 5.00 kPa
• Measurements and prediction of ternary liquid-liquid equilibria for mixtures of IL + sulfur compound + hexadecane
• Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
• Evaluation of 1-ethyl-3-methylimidazolium methylsulfate and 1,3-dimethylimidazolium methylsulfate as solvents for extraction of alkylbenzenes from hexadecane at 313 and 333 K
• Liquid density measurements of cumene, tert-butylbenzene, and hexadecane over wide ranges of temperature and pressure
• A systematic study on volumetric and transport properties of binary systems 1-propanol + n-hexadecane, 1-butanol + n-hexadecane and 1-propanol + ethyl oleate at different temperatures: Experimental and modeling
• Experimental measurement and thermodynamic modeling of phase equilibria of {CO2 + tetralin + n-alkanes (with n = 6, 16)} and its binary systems
• Ternary (liquid + liquid) equilibria for mixtures of 1-hexyl-3-methylimidazolium (tetrafluoroborate or hexafluorophosphate) + benzene + an alkane at T = 298.2 K and p = 0.1 MPa
• Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
• Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
• Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
• Studies of mixing properties of binary systems of 2-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K
• Volumetric, transport, and acoustic properties of binary mixtures of 2-methyl-1-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K: Experimental results, correlation, and prediction by the ERAS model
• Density and speed of sound measurements of hexadecane
• Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
• Excess molar enthalpies of binary mixtures containing 2-decanone or dipentyl ether with long-chain n-alkanes at T = 298.15 K
• Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
• Viscosity of n-hexadecane, n-octadecane and n-eicosane at pressures up to 243 MPa and temperatures up to 534 K
• Experimental high pressure speed of sound and density of (tetralin + n-decane) and (tetralin + n-hexadecane) systems and thermodynamic modeling
• Experimental measurement and prediction of (liquid + liquid + liquid) equilibrium for the system (n-hexadecane + water + triacetin)
• High pressure speed of sound and density of (decalin + n-decane), (decalin + n-hexadecane) and (n-decane + n-hexadecane) systems and thermodynamic modeling with PHCT equation of state
• Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
• Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
• Improving a variation of the DSC technique for measuring the boiling points of pure compounds at low pressures
• Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
• Determination of melting temperatures in hydrocarbon mixtures by differential scanning calorimetry
• Heat capacity and Joule-Thomson coefficient of selected n-alkanes at 0.1 and 10 MPa in broad temperature ranges
• Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
• Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane + two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K
• Ternary liquid-liquid phase equilibria of {ionic liquid + thiophene + (octane/hexadecane)}
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• A simple method to determine the specific volumes of liquids and melts as a function of the temperature. Application to four n-alkanes (C16H34, C18H38, C19H40 and C21H44) under saturating vapour pressure in the 298-573K range
• Express thermo-gravimetric method for the vaporization enthalpies appraisal for very low volatile molecular and ionic compounds.
• Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
• Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
• Silver incorporated microencapsulation of n-hexadecane and noctadecane appropriate for dynamic thermal management in textiles
• Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
• Densities of the binary systems n-hexane + n-decane and nhexane + n-hexadecane up to 60 MPa and 463 K
• Liquid Liquid Equilibria of Binary and Ternary Systems Methanol/Water + n-Hexane, + n-Octane, + n-Dodecane, and + n-Hexadecane in the Temperature Range between T = 283.15 K and T = 333.15 K
• Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylbenzene + Linear Alkanes (n-Decane, n-Dodecane, n-Tetradecane, n-Hexadecane, or n-Heptadecane) at 0.1 MPa
• Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
• Liquid Liquid Equilibria for Systems Containing 4-Phenylbutan-2-one or Benzyl Ethanoate and Selected Alkanes
• Densities and Viscosities at 293.15 373.15 K, Speeds of Sound and Bulk Moduli at 293.15 333.15 K, Surface Tensions, and Flash Points of Binary Mixtures of n-Hexadecane and Alkylbenzenes at 0.1 MPa
• Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
• Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
• Synthesis and Physical and Thermodynamic Properties of Lactic Acid and Malic Acid-Based Natural Deep Eutectic Solvents
• Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
• Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
• Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
• Viscosities of Liquid Hexadecane at Temperatures between 323 K and 673 K and Pressures up to 4 MPa Measured Using a Dual-Capillary Viscometer
• Density and Volumetric Properties of Binary Mixtures of CO2 + Hexadecane from (303.2 to 473.2) K and Pressures up to 50.0 MPa
• Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
• Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
• Fixed-Path Length Laser-Induced Sound Pinging: A Streamlined Method for Sound Speed Determination in Arbitrary Liquids
• Liquid Viscosity and Surface Tension of n-Hexane, n-Octane, n-Decane, and n-Hexadecane up to 573 K by Surface Light Scattering
• Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
• Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
• Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
• Temperature Dependence of Speed of Sound, Densities, and Isentropic Compressibilities of Hexane + Hexadecane, In the Range (293.15 to 373.15) K
• Liquid-Liquid Equilibria for Ternary Mixtures (an Ionic Liquid + Benzene +Heptane or Hexadecane) at T ) 298.2 K and Atmospheric Pressure
• Liquid-Liquid Equilibria Measurements for Ternary System of Hexadecane + 1,3,5-Trimethylbenzene + N-Methyl-2-pyrrolidone
• High-Pressure Density Measurements for the Binary System Cyclohexane + n-Hexadecane in the Temperature Range of (318.15 to 413.15) K
• Liquid-Liquid Equilibria for the Ternary System Water + Hexadecane + Propylene Glycol n-Propyl Ether
• Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
• Vapor Liquid Phase Equilibria and Physical Properties Measurements for Ternary Systems (Methane + Decane + Hexadecane)
• Temperature and Composition Effect on CO2 Miscibility by Interfacial Tension Measurement
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Direct Sugar to Hydrocarbon Diesel (DSH-76) and Binary Mixtures of N-Hexadecane and 2,2,4,6,6-Pentamethylheptane
• Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
• Liquid-Liquid Equilibria for Binary System of Ethanol + Hexadecane at Elevated Temperature and the Ternary Systems of Ethanol + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
• Solid-Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents
• Temperature and Composition Dependence of the Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of 1-Butanol with Hexadecane and Squalane
• Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
• Binary Liquid-Liquid Equilibrium (LLE) for N-Methylformamide (NMF) + Hexadecane between (288.15 and 318.15) K and Ternary LLE for Systems of NMF + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
• Solubility of Carbon Dioxide in Water and Hexadecane: Experimental Measurement and Thermodynamic Modeling
• High-Pressure Viscosity Measurements for the Binary System Cyclohexane + n-Hexadecane in the Temperature Range of (318.15 to 413.15) K
• Excess Molar Enthalpies of Binary Systems of 2-Octanone or 3-Octanone with Dodecane, Tetradecane, or Hexadecane at 298.15 K
• Excess Molar Enthalpies of Binary Systems of n-Valeric Anhydride or n-Hexanoic Anhydride with n-Dodecane, n-Tetradecane, or n-Hexadecane at 298.15 K
• (Liquid + Liquid) Equilibrium for (N,N-Dimethylformamide (DMF) + Hexadecane) at Temperatures between (293.15 and 313.15) K and Ternary Mixtures of (DMF + Hexadecane) with Either Quinoline, or Pyridine, or Pyrrole, or Aniline, or Indole at T = 298.15 K
• Experimental Measurement and Thermodynamic Modeling for the Solubility of Methane in Water and Hexadecane
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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Outlier This icon means that the value is more than 2 standard deviations away from the property mean.